CN108355503A - A kind of food emulsion shearing homogenizer and its technique - Google Patents
A kind of food emulsion shearing homogenizer and its technique Download PDFInfo
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- CN108355503A CN108355503A CN201810242631.2A CN201810242631A CN108355503A CN 108355503 A CN108355503 A CN 108355503A CN 201810242631 A CN201810242631 A CN 201810242631A CN 108355503 A CN108355503 A CN 108355503A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/41—Emulsifying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/44—Mixers in which the components are pressed through slits
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/074—Stirrers characterised by their mounting on the shaft having two or more mixing elements being concentrically mounted on the same shaft
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1125—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis
- B01F27/11251—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis having holes in the surface
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/19—Stirrers with two or more mixing elements mounted in sequence on the same axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
- B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Colloid Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention discloses a kind of food emulsions to shear homogenizer, including is shell stator, the first rotor and the second rotor；Shell stator is the closed column-shaped barrel of vertical posture, and the lower end of the shell stator connects gum feed pipe, and shell stator upper end side wall connects discharge nozzle；The first rotor is concentric in the shell bore of stator, and the second rotor coaxial heart is in the first rotor inner cavity；First motor drives the first rotor to be rotated along axis, secondly motor drives second rotor to be rotated along axis；Wherein the first rotor and bitrochanteric rotation direction is opposite；The structure of the present invention is simple, make basic lotion and addition solution that interlaced liquid motion occur in its emulsifying homogeneous tank body, and then keeping the drop of compound body fluid finer and smoother, particle diameter distribution is narrower, thus forms mixed liquor stability preferably blending property compound body fluid.
Description
Technical field
The invention belongs to colloid homogenization field more particularly to a kind of food emulsion shearing homogenizer and its works
Skill.
Background technology
The pasty masses such as cream, emulsion generally require to need addition portion in process to improve product quality
Additive solution, traditional mixing arrangement is divided to be difficult to realize the fully dispersed auger of solution in pasty masses.
Invention content
Goal of the invention：In order to overcome the deficiencies in the prior art, present invention offer discharging is finer and smoother, and annex solution melts
Close a kind of more uniform food emulsion shearing homogenizer and its technique.
Technical solution：To achieve the above object, a kind of food emulsion of the invention shears homogenizer, including is shell
Stator, the first rotor and the second rotor；Shell stator is the closed column-shaped barrel of vertical posture, the lower end of the shell stator
Gum feed pipe is connected, shell stator upper end side wall connects discharge nozzle；The first rotor is concentric fixed in the shell
Sub- inner cavity, the second rotor coaxial heart is in the first rotor inner cavity；First motor drives the first rotor to be revolved along axis
Turn, secondly motor drives second rotor to be rotated along axis；Wherein the first rotor and bitrochanteric rotation direction is opposite.
Further, the first rotor is by the first rotating shaft of concentric setting, the first shearing porose disc, the second shearing perforation
Disk, the first cylinder, the second cylinder, the first connection pipe body and the second connection pipe body are constituted；
The first motor is drivingly connected in the first rotating shaft lower end；The first rotating shaft upper end is rotatable stretch into it is described
In shell stator, the first rotating shaft upper end is fixedly connected with the first cylinder, first cylinder upper end is fixedly connected with the first connection
Tube body, first connection pipe body upper end are fixedly connected with the second cylinder, and second cylinder upper end is fixedly connected with the second connecting tube
Body, second connection pipe body upper end are fixedly connected with the second shearing porose disc；
The inside of first cylinder and the second cylinder is respectively the first column chamber and the second column chamber, first connection pipe body
The first interior axocoel upper and lower side is respectively communicated with the first column chamber and the second column chamber, the second axocoel in second connection pipe body
Lower end is connected to the second column chamber；The cylindrical outer wall of first cylinder and the second cylinder and the inner wall of the shell stator can turn
Dynamic clearance fit；
The first shearing porose disc and the second shearing porose disc are disc structure, and the first shearing porose disc is fixedly installed on institute
It states in first rotating shaft, and the first shearing porose disc, between first cylinder and shell bore of stator bottom surface, described second cuts
Cut hole disk is between second cylinder and shell bore of stator top surface；The first shearing porose disc and second shears porose disc
The rotatable clearance fit of inner wall of outer ring and the shell stator；
It is described first shearing porose disc and between shell bore of stator bottom surface formed feed cavity, it is described first shearing porose disc with
The first homogeneous chamber is formed between first cylinder, and the second homogeneous chamber is formed between second cylinder and the first cylinder, it is described
Third homogeneous chamber is formed between second shearing porose disc and second cylinder, described second shears in porose disc and the shell stator
Chamber forms discharging chamber between top surface；The discharging chamber conducting connects the discharge nozzle, the feed cavity conducting connection gum feed
Pipe；
It is evenly equipped with first group of shearing perforation on the first shearing porose disc, the first column chamber lower wall hollow out has been uniformly arranged the
Two groups of shearing perforations, the first column chamber upper wall hollow out are evenly equipped with third group shearing perforation, and the second column chamber lower wall hollow out is laid
It is equipped with the 4th group of shearing perforation, the second column chamber upper wall hollow out has been uniformly arranged the 5th group of shearing perforation, the second shearing porose disc
Upper hollow out is evenly equipped with the 6th group of shearing perforation.
Further, further include the first homogeneous blade, the second homogeneous blade and third homogeneous blade；Three pieces are vertically arranged
First homogeneous blade is located in the first homogeneous chamber, and circumferentially array is connected to described first turn to the first homogeneous of three pieces blade
Axis outer wall；The second vertically arranged homogeneous blade of three pieces is located in the second homogeneous chamber, and three pieces the second homogeneous blade is in circle
All arrays are connected to the first rotating shaft outer wall；The vertically arranged third homogeneous blade of three pieces is located in the third homogeneous chamber,
And circumferentially array is connected to the first rotating shaft outer wall to three pieces third homogeneous blade；The first homogeneous blade, the second homogeneous
Blade and third homogeneous blade are rectangular paddle, and array is provided on the space of a whole page of the close first rotating shaft axis of the rectangular paddle
The space of a whole page of several hollow holes, the separate first rotating shaft axis of the rectangular paddle is in comb teeth-shaped.
Further, second rotor is made of the second shaft of concentric setting, annex solution funnel and conduction column；Institute
The second motor is stated to be drivingly connected in second shaft upper end；It is fixedly installed horizontally-supported disk on the inside of the annex solution funnel,
Second shaft lower end is concentric to be fixedly connected with the horizontally-supported disk, and the disk of the horizontally-supported disk is provided with leakage
Hole, annex solution funnel lower end are fixedly connected with the conduction column, and the conduction column is internally provided with the first annex solution channel；Institute
State the liquid outlet that the conducting of the first annex solution channel upper end connects annex solution funnel lower end；It rotatably stretches the conduction column lower end
Enter in the shell stator, and activity is worn into the second axocoel, the second column chamber, the first axocoel and the first column the conduction column successively
Chamber；Second group of agitation blades and first group of agitation blades are fixedly installed on the post jamb of the conduction column respectively；Described second group
Agitation blades and first group of agitation blades are located in the second column chamber and the first column chamber.
Further, be provided with the second annex solution channel in the first rotating shaft, second annex solution channel upper end from
The first rotating shaft upper end is pierced by；Second annex solution channel lower end inner wall is provided with several fluid holes, each fluid hole
Outlet be located in the feed cavity；The first rotating shaft upper end is concentric to be provided with round recessed；The conduction column lower end is same
Axle center is rotatably inserted into the round recessed, and second annex solution channel is with first annex solution channel in the round recessed
Place's conducting connection.
Further, the upper lower wall of the first column chamber and the second column chamber is to the thin-wall construction of millimeter, and described first cuts
Cut hole disk and the second shearing porose disc are to the thin-wall construction of millimeter.
Further, a kind of colloid emulsion shears homogenization：
Simultaneously start first motor and the second motor, make the first rotor and the second rotor start to rotate, and the first rotor and
Bitrochanteric rotation direction is opposite；Thick base gel liquid continues through gum feed pipe under the action of pump and adds to
In feed cavity, then, a certain amount of additive solution is poured into annex solution funnel, and remain addition in the follow-up process
Contain additive solution in liquid funnel, the additive solution in annex solution funnel flows to the second addition along the first annex solution channel
Liquid channel is further flowed out in feed cavity by several fluid holes of the second annex solution channel lower end, due in feed cavity
Full of sticky base gel liquid, but highly higher than shell bore of stator top place due to height where annex solution funnel,
Therefore the higher pressure in feed cavity of pressure at fluid hole, therefore additive solution can continuously slowly be flowed out from fluid hole
Into feed cavity, and tentatively merged with base gel liquid in feed cavity；As base gel liquid is accumulated in feed cavity, make charging
Liquid level is gradually increasing until first shears height where porose disc, with continuing to build up for base gel liquid, feed cavity top in chamber
Colloid tentatively merge liquid through first shearing porose disc on several first group of shearing perforation, be expressed into first in shape of squeezing toothpaste out of a tube
It is freshly extruded in the first homogeneous chamber under the effect of the continuous rotation of the first homogeneous blade in the first homogeneous chamber in homogeneous chamber
Colloid tentatively merges liquid by radially continuous shear stress is broken up rapidly, then as the colloid mixed liquor in the first homogeneous chamber by
It gradually accumulates, the space of a whole page further shears the colloid mixed liquor in its first homogeneous chamber in the first homogeneous blade of comb teeth-shaped
And mixing, so that base gel liquid and additive solution in colloid mixed liquor is tentatively uniformly mixed, at this time also in uniform mixing
State, the also not up to completely mutual peptization of base gel liquid and additive solution, at the same time in the drive of the first homogeneous blade
Colloid mixed liquor in lower first homogeneous chamber starts to rotate synchronously；At this time as the colloid mixed liquor in the first homogeneous chamber continues to tire out
Product, the colloid mixed liquor of the first homogeneous chamber upper end rotated start to penetrate progressively through several second groups on the first column chamber lower wall
Shearing perforation is simultaneously squeezed into the first column chamber, does continuous rotation fortune in the first column chamber column chamber due to first group of agitation blades at this time
It is dynamic, and its rotary motion direction with the rotary motion direction in the first homogeneous chamber conversely, because the colloid in the first column chamber mixes
Liquid is dry when being squeezed into the first column chamber, and the colloidal solution in the first column chamber is expressed into still from second group of shearing perforation under effect of inertia
Original movement tendency is so remain, due to the agitation direction of suffered first group of agitation blades in the first column chamber and from second group
Shearing perforation squeeze out colloidal solution movement tendency direction on the contrary, at this time second group of shearing perforation be expressed into the colloidal solution in the first column chamber by
To dual strong shear effect, the colloidal solution in the first column chamber is at the same time entered under the action of first group of agitation blades
High speed rotary motion is done, since the inner wall direction of rotation of the first column chamber and the direction of rotation of first group of agitation blades are on the contrary, in turn
Make the colloid mixed liquor in the first column chamber at inner wall that the movement opposite with first group of agitation blades can occur, and then makes first
Interlaced liquid motion occurs in column chamber, and then keeps the drop of epoxy glue body fluid finer and smoother, particle diameter distribution is narrower, thus
Mixed liquor stability preferably blending property epoxy glue body fluid is formed in first column chamber；It is mixed in the first column chamber according to above-mentioned rule
Colloidal solution is closed gradually to be squeezed into the second homogeneous chamber with the accumulation of liquid, with the further supply of base gel liquid,
The colloidal solution that mixing is further emulsified in second homogeneous chamber is squeezed into the second column chamber, further emulsification mixing in the second column chamber
Colloidal solution be squeezed into third homogeneous chamber, in final third homogeneous chamber by fully refinement homogeneous colloid mixed liquor be squeezed into
Into discharging chamber, finally overflows or be pumped out into discharge nozzle.
Advantageous effect：The structure of the present invention is simple, makes basic lotion and addition solution that phase occur in its emulsifying homogeneous tank body
Mutually liquid motion staggeredly, and then keep the drop of compound body fluid finer and smoother, particle diameter distribution is narrower, thus forms mixed liquor and stablize
The better blending property compound body fluid of property.
Description of the drawings
Attached drawing 1 is integral outer structural schematic diagram of the present invention；
Attached drawing 2 is entirety sectional view of the present invention；
Attached drawing 3 is the first rotor and the second rotor assembled state structural schematic diagram；
Attached drawing 4 is the first rotor structural schematic diagram；
Attached drawing 5 is the partial schematic diagram of attached drawing 3；
Attached drawing 6 is that schematic diagram is cut inside the first rotor；
Attached drawing 7 is the second rotor schematic diagram.
Specific implementation mode
The present invention is further described below in conjunction with the accompanying drawings.
As shown in attached drawing 1 to 7, a kind of food emulsion shears homogenizer, including be shell stator 6, the first rotor and
Second rotor；Shell stator 6 is the closed column-shaped barrel of vertical posture, and the lower end of the shell stator 6 connects gum feed pipe
34,6 upper end side wall of the shell stator connects discharge nozzle 33；The first rotor is concentric in 6 inner cavity of shell stator, institute
The second rotor coaxial heart is stated in the first rotor inner cavity；First motor drives the first rotor to be rotated along axis, secondly electric
Machine drives second rotor to be rotated along axis；Wherein the first rotor and bitrochanteric rotation direction is opposite.
The first rotor shears porose disc 44, second by the first rotating shaft 16, first of concentric setting and shears porose disc 21, the
One cylinder 29, the second cylinder 25, the first connection pipe body 38 and the second connection pipe body 39 are constituted；
The first motor is drivingly connected in 16 lower end of the first rotating shaft；16 upper end of the first rotating shaft is rotatable to be stretched into
In the shell stator 6,16 upper end of the first rotating shaft is fixedly connected with the first cylinder 29,29 upper end of the first cylinder is fixed and connected
The first connection pipe body 38 is connect, 38 upper end of the first connection pipe body is fixedly connected with the second cylinder 25,25 upper end of the second cylinder
It is fixedly connected with the second connection pipe body 39,39 upper end of the second connection pipe body is fixedly connected with the second shearing porose disc 21；
The inside of first cylinder, 29 and second cylinder 25 is respectively the first column chamber 12 and the second column chamber 24, and described first
41 upper and lower side of the first axocoel in connection pipe body 38 is respectively communicated with the first column chamber 12 and the second column chamber 24, second connection
42 lower end of the second axocoel in tube body 39 is connected to the second column chamber 24；Outside the cylinder of first cylinder, 29 and second cylinder 25
The rotatable clearance fit of inner wall of wall and the shell stator 6；
It is disc structure that the first shearing porose disc 44 and second, which shears porose disc 21, and the first shearing fixation of porose disc 44 is set
Be placed in the first rotating shaft 16, and the first shearing porose disc 44 be located at first cylinder 29 and 6 inner chamber bottom surface of shell stator it
Between, the second shearing porose disc 21 is located between 6 inner cavity top surface of second cylinder 25 and shell stator；First shearing perforation
Disk 44 and second shears the rotatable clearance fit of inner wall of the outer ring and the shell stator 6 of porose disc 21；
The first shearing porose disc 44 and formation feed cavity 15, first shearing between 6 inner chamber bottom surface of shell stator
The first homogeneous chamber 30 is formed between porose disc 44 and first cylinder 29, is formed between second cylinder, 25 and first cylinder 29
Second homogeneous chamber 28, formation third homogeneous chamber 23 between the second shearing porose disc 21 and second cylinder 25, described second
It shears and forms discharging chamber 4 between porose disc 21 and 6 inner cavity top surface of the shell stator；The conducting of the discharging chamber 4 connects the discharging
Pipe 33, the conducting connection gum feed of the feed cavity 15 pipe 34；
It is evenly equipped with first group of shearing perforation 43 on the first shearing porose disc 44, the 12 lower wall hollow out of the first column chamber is laid
It is equipped with second group of shearing perforation 13, the 12 upper wall hollow out of the first column chamber is evenly equipped with third group shearing perforation 10, the second column chamber 24
Lower wall hollow out has been uniformly arranged the 4th group of shearing perforation 26, and the 24 upper wall hollow out of the second column chamber has been uniformly arranged the 5th group of shearing perforation
7, described second, which shears hollow out on porose disc 21, is evenly equipped with the 6th group of shearing perforation 21.
Further include the first homogeneous blade 31, the second homogeneous blade 27 and third homogeneous blade 22；Three pieces it is vertically arranged
One homogeneous blade 31 is located in the first homogeneous chamber 30, and circumferentially array is connected to described to the first homogeneous of three pieces blade 31
One shaft, 16 outer wall；The second vertically arranged homogeneous blade 27 of three pieces is located in the second homogeneous chamber 28, and three pieces second are equal
Circumferentially array is connected to 16 outer wall of the first rotating shaft to matter blade 27；The vertically arranged third homogeneous blade 22 of three pieces is located at institute
It states in third homogeneous chamber 23, and circumferentially array is connected to 16 outer wall of the first rotating shaft to three pieces third homogeneous blade 22；It is described
First homogeneous blade 31, the second homogeneous blade 27 and third homogeneous blade 22 are rectangular paddle, the rectangular paddle close to the
Array is provided with several hollow holes 35 on the space of a whole page of one shaft, 16 axis, 16 axis of separate first rotating shaft of the rectangular paddle
The space of a whole page is in 36 shape of broach.
Second rotor is made of the second shaft 17, annex solution funnel 1 and the conduction column 40 of concentric setting；Described
Two motors are drivingly connected in 17 upper end of the second shaft；1 inside of the annex solution funnel is fixedly installed horizontally-supported disk 2,
Second shaft, 17 lower end is concentric to be fixedly connected with the horizontally-supported disk 18, and the disk of the horizontally-supported disk 18 is provided with
Liquid-leaking nozzle 2,1 lower end of annex solution funnel are fixedly connected with the conduction column 40, and the conduction column 40 is internally provided with first and adds
Liquid feeding channel 3；The conducting of first annex solution channel, 3 upper end connects the liquid outlet of 1 lower end of annex solution funnel；The conducting
40 lower end of column is rotatably stretched into the shell stator 6, and activity is worn into the second axocoel 42, second conduction column 40 successively
Column chamber 24, the first axocoel 41 and the first column chamber 12；It is fixedly installed second respectively on the post jamb of the conduction column 40
Group agitation blades 8 and first group of agitation blades 11；Second group of agitation blades 8 and first group of agitation blades 11 are located at institute
It states in the second column chamber 24 and the first column chamber 12.
It is provided with the second annex solution channel 14 in the first rotating shaft 16, second annex solution channel, 14 upper end is from described
16 upper end of first rotating shaft is pierced by；Second annex solution channel, 14 lower end inner wall is provided with several fluid holes 32, it is each it is described go out liquid
The outlet in hole 32 is located in the feed cavity 15；16 upper end of the first rotating shaft is concentric to be provided with round recessed 37；It is described to lead
40 lower end of through post is concentric to be rotatably inserted into the round recessed 37, second annex solution channel 14 and first annex solution
Connection is connected in channel 3 at the round recessed 37.
The thin-wall construction that the upper lower wall of the first column chamber 12 and the second column chamber 24 is 1 to 2 millimeter, first shearing perforation
Disk 44 and second shears the thin-wall construction that porose disc 21 is 1 to 2 millimeter.
The method, process and technological progress of this programme arrange as follows：
Simultaneously start first motor and the second motor, make the first rotor and the second rotor start to rotate, and the first rotor and
Bitrochanteric rotation direction is opposite；Thick base gel liquid continues through the supplement of gum feed pipe 34 under the action of pump
Into feed cavity 15, then, a certain amount of additive solution is poured into annex solution funnel 1, and protects always in the follow-up process
It holds and contains additive solution in annex solution funnel 1, the additive solution in annex solution funnel 1 is flowed along the first annex solution channel 3
To the second annex solution channel 14, further feed cavity is flowed out to by several fluid holes 32 of 14 lower end of the second annex solution channel
In 15, due to being full of sticky base gel liquid in feed cavity 15, but since height where annex solution funnel 1 is fixed higher than shell
Height where sub 6 inner cavity tops, therefore the higher pressure in feed cavity 15 of pressure at fluid hole 32, therefore additive solution
It can continuously slowly flow out in feed cavity 15 from fluid hole 32, and tentatively be merged with base gel liquid in feed cavity 15；With
Base gel liquid is accumulated in feed cavity 15, and liquid level in feed cavity 15 is made to be gradually increasing until high where the first shearing porose disc 44
Degree, with continuing to build up for base gel liquid, the colloid on 15 top of feed cavity tentatively merges liquid through on the first shearing porose disc 44
Several first group of shearing perforation 43, be expressed into the first homogeneous chamber 30 in shape of squeezing toothpaste out of a tube, in the first homogeneous chamber 30
Under the continuous rotation effect of one homogeneous blade 31, the freshly extruded colloid in the first homogeneous chamber 30 tentatively merges liquid by rapidly along diameter
It breaks up to direction continuous shear stress, is built up then as the colloid mixed liquor in the first homogeneous chamber 30, the space of a whole page is in 36 shape of broach
The first homogeneous blade 31 the colloid mixed liquor in its first homogeneous chamber 30 is further sheared and mixing, keep colloid mixed
The base gel liquid and additive solution closed in liquid tentatively uniformly mixes, at this time also in uniform admixture, also not up to base
Plinth colloidal solution and the completely mutual peptization of additive solution, the at the same time first homogeneous chamber 30 under the drive of the first homogeneous blade 31
In colloid mixed liquor start to rotate synchronously；At this time as the colloid mixed liquor in the first homogeneous chamber 30 continues to build up, first
The colloid mixed liquor of 3 upper end of matter chamber rotated starts to penetrate progressively through several second group of shearing perforation on 12 lower wall of the first column chamber
It 13 and is squeezed into the first column chamber 12, does continuous rotation fortune in 12 column chamber of the first column chamber due to first group of agitation blades 11 at this time
It is dynamic, and its rotary motion direction with the rotary motion direction in the first homogeneous chamber 30 conversely, because colloid in the first column chamber 12
Mixed liquor is dry when being squeezed into the first column chamber 12, is expressed into the first column chamber 12 from second group of shearing perforation 13 under effect of inertia
Colloidal solution still maintain original movement tendency, due to the agitation of suffered first group of agitation blades 11 in the first column chamber 12
Direction with from the colloidal solution movement tendency direction that second group of shearing perforation 13 squeezes out on the contrary, second group of shearing perforation 13 is expressed into the at this time
By dual strong shear effect, the colloidal solution at the same time entered in the first column chamber 12 exists colloidal solution in one column chamber 12
High speed rotary motion is done under the action of first group of agitation blades 11, since the inner wall direction of rotation of the first column chamber 12 is stirred with first group
The direction of rotation of movable vane piece 11 on the contrary, make the colloid mixed liquor in the first column chamber 12 at inner wall that can occur and first group in turn
The opposite movement of agitation blades 11, and then make that interlaced liquid motion occurs in the first column chamber 12, and then make colloid mixture
The drop of liquid is finer and smoother, and particle diameter distribution is narrower, thus preferably blending property is mixed for formation mixed liquor stability in the first column chamber 12
Close colloidal solution；According to above-mentioned rule, the epoxy glue body fluid in the first column chamber 12 is gradually squeezed into second with the accumulation of liquid
In homogeneous chamber 28, with the further supply of base gel liquid, the colloidal solution of mixing is further emulsified in the second homogeneous chamber 28
It is squeezed into the second column chamber 24, the colloidal solution that mixing is further emulsified in the second column chamber 24 is squeezed into third homogeneous chamber 23
In, be squeezed into discharging chamber 4 by the colloid mixed liquor of fully refinement homogeneous in final third homogeneous chamber 23, it is final overflow or by
In pumped to discharge nozzle 33.
The above is only a preferred embodiment of the present invention, it should be pointed out that：For the ordinary skill people of the art
For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also answered
It is considered as protection scope of the present invention.
Claims (7)
1. a kind of food emulsion shears homogenizer, it is characterised in that：Including being shell stator (6), the first rotor and second
Rotor；Shell stator (6) is the closed column-shaped barrel of vertical posture, and the lower end of the shell stator (6) connects gum feed pipe
(34), shell stator (6) upper end side wall connection discharge nozzle (33)；The first rotor is concentric in the shell stator
(6) inner cavity, the second rotor coaxial heart is in the first rotor inner cavity；First motor drives the first rotor to be revolved along axis
Turn, secondly motor drives second rotor to be rotated along axis；Wherein the first rotor and bitrochanteric rotation direction is opposite.
2. a kind of food emulsion according to claim 1 shears homogenizer, it is characterised in that：The first rotor by
The first rotating shaft (16) of concentric setting, the first shearing porose disc (44), the second shearing porose disc (21), the first cylinder (29), second
Cylinder (25), the first connection pipe body (38) and the second connection pipe body (39) are constituted；
The first motor is drivingly connected in the first rotating shaft (16) lower end；First rotating shaft (16) upper end is rotatable to be stretched into
In the shell stator (6), first rotating shaft (16) upper end is fixedly connected with the first cylinder (29), on first cylinder (29)
End is fixedly connected with the first connection pipe body (38), and the first connection pipe body (38) upper end is fixedly connected with the second cylinder (25), described
Second cylinder (25) upper end is fixedly connected with the second connection pipe body (39), and the second connection pipe body (39) upper end is fixedly connected with second
Shear porose disc (21)；
The inside of first cylinder (29) and the second cylinder (25) is respectively the first column chamber (12) and the second column chamber (24), described
The first axocoel (41) upper and lower side in first connection pipe body (38) is respectively communicated with the first column chamber (12) and the second column chamber (24),
The second axocoel (42) lower end in second connection pipe body (39) is connected to the second column chamber (24)；First cylinder (29)
With the rotatable clearance fit of inner wall of the cylindrical outer wall and the shell stator (6) of the second cylinder (25)；
The first shearing porose disc (44) and the second shearing porose disc (21) are disc structure, and the first shearing porose disc (44) is fixed
It is set in the first rotating shaft (16), and the first shearing porose disc (44) is located at first cylinder (29) and shell stator (6)
Between inner chamber bottom surface, the second shearing porose disc (21) be located at second cylinder (25) and shell stator (6) inner cavity top surface it
Between；The outer ring and the inner wall of the shell stator (6) of the first shearing porose disc (44) and the second shearing porose disc (21) are rotatable
Clearance fit；
The first shearing porose disc (44) and feed cavity (15) is formed between shell stator (6) inner chamber bottom surface, described first is cut
The first homogeneous chamber (30), second cylinder (25) and the first cylinder are formed between cut hole disk (44) and first cylinder (29)
(29) the second homogeneous chamber (28) is formed between, and third is formed between the second shearing porose disc (21) and second cylinder (25)
Homogeneous chamber (23), second shearing form discharging chamber (4) between porose disc (21) and the shell stator (6) inner cavity top surface；Institute
It states discharging chamber (4) conducting and connects the discharge nozzle (33), feed cavity (15) the conducting connection gum feed pipe (34)；
It is evenly equipped with first group of shearing perforation (43) on the first shearing porose disc (44), the first column chamber (12) lower wall hollow out is uniformly distributed
It is provided with second group of shearing perforation (13), the first column chamber (12) upper wall hollow out is evenly equipped with third group shearing perforation (10), and described
Two column chamber (24) lower wall hollow outs have been uniformly arranged the 4th group of shearing perforation (26), and the second column chamber (24) upper wall hollow out is uniformly arranged
There is the 5th group of shearing perforation (7), described second, which shears hollow out on porose disc (21), is evenly equipped with the 6th group of shearing perforation (21).
3. a kind of food emulsion according to claim 2 shears homogenizer, it is characterised in that：It further include the first homogeneous
Blade (31), the second homogeneous blade (27) and third homogeneous blade (22)；First vertically arranged homogeneous blade (31) position of three pieces
In the first homogeneous chamber (30), and circumferentially array is connected to the first rotating shaft (16) to three pieces the first homogeneous blade (31)
Outer wall；The second vertically arranged homogeneous blade (27) of three pieces is located in the second homogeneous chamber (28), and three pieces the second homogeneous leaf
Circumferentially array is connected to the first rotating shaft (16) outer wall to piece (27)；The vertically arranged third homogeneous blade (22) of three pieces is located at
In the third homogeneous chamber (23), and circumferentially array is connected to the first rotating shaft (16) outside to three pieces third homogeneous blade (22)
Wall；The first homogeneous blade (31), the second homogeneous blade (27) and third homogeneous blade (22) are rectangular paddle, the rectangle
Array is provided with several hollow holes (35) on the space of a whole page of close first rotating shaft (16) axis of blade, the rectangular paddle it is separate
The space of a whole page of first rotating shaft (16) axis is in broach (36) shape.
4. a kind of food emulsion according to claim 2 shears homogenizer, it is characterised in that：Second rotor by
The second shaft (17), annex solution funnel (1) and the conduction column (40) of concentric setting are constituted；Second motor be drivingly connected in
Second shaft (17) upper end；It is fixedly installed horizontally-supported disk (2) on the inside of the annex solution funnel (1), described second turn
Axis (17) lower end is concentric to be fixedly connected with the horizontally-supported disk (18), and the disk of the horizontally-supported disk (18) is provided with leakage
Hole (2), annex solution funnel (1) lower end are fixedly connected with the conduction column (40), and the conduction column (40) is internally provided with
One annex solution channel (3)；First annex solution channel (3) upper end conducting connection annex solution funnel (1) lower end goes out liquid
Mouthful；Conduction column (40) lower end is rotatably stretched into the shell stator (6), and activity is worn the conduction column (40) successively
Enter the second axocoel (42), the second column chamber (24), the first axocoel (41) and the first column chamber (12)；On the post jamb of the conduction column (40)
It is fixedly installed second group of agitation blades (8) and first group of agitation blades (11) respectively；Second group of agitation blades (8) and
One group of agitation blades (11) is located in the second column chamber (24) and the first column chamber (12).
5. a kind of food emulsion according to claim 4 shears homogenizer, it is characterised in that：The first rotating shaft
(16) the second annex solution channel (14) is provided in, second annex solution channel (14) upper end is from the first rotating shaft (16)
End is pierced by；Second annex solution channel (14) lower end inner wall is provided with several fluid holes (32), each fluid hole (32)
Outlet is located in the feed cavity (15)；First rotating shaft (16) upper end is concentric to be provided with round recessed (37)；It is described to lead
Through post (40) lower end is concentric to be rotatably inserted into the round recessed (37), second annex solution channel (14) and described first
Connection is connected in annex solution channel (3) at the round recessed (37).
6. a kind of food emulsion according to claim 2 shears homogenizer, it is characterised in that：The first column chamber
(12) and the upper lower wall of the second column chamber (24) is 1 to 2 millimeter of thin-wall construction, and described first shears porose disc (44) and the second shearing
The thin-wall construction that porose disc (21) is 1 to 2 millimeter.
7. shearing homogenization according to a kind of colloid emulsion of any one of claim 1 to 6, it is characterised in that：
Start first motor and the second motor simultaneously, makes the first rotor and the second rotor start to rotate, and the first rotor and second
The rotation direction of rotor is opposite；Thick base gel liquid continues through gum feed pipe (34) under the action of pump and adds to
In feed cavity (15), then, a certain amount of additive solution is poured into annex solution funnel (1), and in the follow-up process always
It keeps containing additive solution in annex solution funnel (1), the additive solution in annex solution funnel (1) is logical along the first annex solution
Road (3) flows to the second annex solution channel (14), further passes through several fluid holes of second annex solution channel (14) lower end
(32) it flows out in feed cavity (15), due to being full of sticky base gel liquid in feed cavity (15), but since annex solution leaks
Height where (1) struggle against higher than height where shell stator (6) inner cavity top, therefore the pressure at fluid hole (32) is higher in charging
Pressure in chamber (15), therefore additive solution continuously can be flowed out to slowly from fluid hole (32) in feed cavity (15), and just
Step is merged with base gel liquid in feed cavity (15)；With the accumulation in feed cavity (15) of base gel liquid, make feed cavity (15)
Middle liquid level is gradually increasing until first shears height where porose disc (44), with continuing to build up for base gel liquid, feed cavity
(15) colloid on top tentatively merges liquid through several first group of shearing perforation (43) on the first shearing porose disc (44), in crowded tooth
Paste is expressed into the first homogeneous chamber (30), and the continuous rotation of the first homogeneous blade (31) in the first homogeneous chamber (30) is made
Under, the freshly extruded colloid in the first homogeneous chamber (30) tentatively merges liquid by radially continuous shear stress is broken up rapidly, so
Afterwards as the colloid mixed liquor in the first homogeneous chamber (30) is built up, the space of a whole page is in the first homogeneous blade (31) of broach (36) shape
Colloid mixed liquor in its first homogeneous chamber (30) is further sheared and mixing, makes the basic glue in colloid mixed liquor
Body fluid and additive solution tentatively uniformly mix, at this time also in uniform admixture, also not up to base gel liquid and addition
The completely mutual peptization of agent solution, at the same time the colloid under the drive of the first homogeneous blade (31) in the first homogeneous chamber (30) is mixed
Liquid is closed to start to rotate synchronously；At this time as the colloid mixed liquor in the first homogeneous chamber (30) continues to build up, on the first homogeneous chamber (3)
The colloid mixed liquor rotated at end starts to penetrate progressively through several second group of shearing perforation (13) on first column chamber (12) lower wall
And be squeezed into the first column chamber (12), continuous rotation is done in first column chamber (12) column chamber due to first group of agitation blades (11) at this time
Transhipment is dynamic, and the rotary motion direction in its rotary motion direction and the first homogeneous chamber (30) is conversely, because the first column chamber (12)
In colloid mixed liquor it is dry when being squeezed into the first column chamber (12), be expressed into from second group of shearing perforation (13) under effect of inertia
Colloidal solution in first column chamber (12) still maintains original movement tendency, due to first group suffered in the first column chamber (12)
The agitation direction of agitation blades (11) with from the colloidal solution movement tendency direction that second group of shearing perforation (13) squeezes out on the contrary, at this time the
Two groups of shearing perforations (13) are expressed into the colloidal solution in the first column chamber (12) by dual strong shear effect, at the same time enter
High speed rotary motion is done under the action of first group of agitation blades (11) to the colloidal solution in the first column chamber (12), due to the first column
The direction of rotation of the inner wall direction of rotation of chamber (12) and first group of agitation blades (11) is on the contrary, make to lean in the first column chamber (12) in turn
The movement opposite with first group agitation blades (11) can occur for the colloid mixed liquor at nearly inner wall, and then make in the first column chamber (12)
Interlaced liquid motion occurs, and then keeps the drop of epoxy glue body fluid finer and smoother, particle diameter distribution is narrower, thus in the first column
Mixed liquor stability preferably blending property epoxy glue body fluid is formed in chamber (12)；According to above-mentioned rule, in the first column chamber (12)
Epoxy glue body fluid is gradually squeezed into the accumulation of liquid in the second homogeneous chamber (28), further with base gel liquid
It supplies, the colloidal solution that mixing is further emulsified in the second homogeneous chamber (28) is squeezed into the second column chamber (24), the second column chamber
(24) colloidal solution that mixing is further emulsified in is squeezed into third homogeneous chamber (23), is filled in final third homogeneous chamber (23)
Divide the colloid mixed liquor of refinement homogeneous to be squeezed into discharging chamber (4), finally overflows or be pumped out into discharge nozzle (33).
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| CN201810242631.2A CN108355503A (en) | 2018-03-23 | 2018-03-23 | A kind of food emulsion shearing homogenizer and its technique |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109395648A (en) * | 2018-09-25 | 2019-03-01 | 崔云华 | A kind of preparation process of water paint, device and its formula |
| CN109401524A (en) * | 2018-09-25 | 2019-03-01 | 崔云华 | A kind of preparation process of water paint, equipment and formula |
| CN111110075A (en) * | 2019-12-02 | 2020-05-08 | 斯贝乐电器（浙江）股份有限公司 | Butter making machine |
| CN113153251A (en) * | 2021-02-07 | 2021-07-23 | 胜利油田胜利泵业有限责任公司 | Rotary shearing type polymer viscosity reduction device |
| CN113208093A (en) * | 2021-04-29 | 2021-08-06 | 焙之道食品(福建)有限公司 | Baking-resistant salad sauce preparation system and preparation method |
| CN113303462A (en) * | 2021-04-29 | 2021-08-27 | 焙之道食品(福建)有限公司 | Bread sandwich salad sauce preparation system and method |
| CN114471208A (en) * | 2022-01-17 | 2022-05-13 | 河南工业大学 | Preparation facilities of liquid dairy products that contains dietary fiber |
| CN114732048A (en) * | 2022-04-25 | 2022-07-12 | 江苏新小莓食品有限公司 | Double-protein milk composite fermentation process |
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| CN102164660A (en) * | 2009-09-28 | 2011-08-24 | 新东工业株式会社 | A device for a continuous dispersion by a strong shearing |
| CN202289945U (en) * | 2011-07-25 | 2012-07-04 | 无锡轻大食品装备有限公司 | Shear dispersion system for high-efficiently mixing viscous materials |
| CN206500067U (en) * | 2016-12-08 | 2017-09-19 | 无锡海特信成高分子科技有限公司 | It is a kind of to be sufficiently stirred for the agitator of adhesive |
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| CN102164660A (en) * | 2009-09-28 | 2011-08-24 | 新东工业株式会社 | A device for a continuous dispersion by a strong shearing |
| CN202289945U (en) * | 2011-07-25 | 2012-07-04 | 无锡轻大食品装备有限公司 | Shear dispersion system for high-efficiently mixing viscous materials |
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Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109395648A (en) * | 2018-09-25 | 2019-03-01 | 崔云华 | A kind of preparation process of water paint, device and its formula |
| CN109401524A (en) * | 2018-09-25 | 2019-03-01 | 崔云华 | A kind of preparation process of water paint, equipment and formula |
| CN109395648B (en) * | 2018-09-25 | 2019-09-17 | 挪亚家家具（广东）有限公司 | A kind of preparation process of water paint, device and its formula |
| CN109401524B (en) * | 2018-09-25 | 2021-04-09 | 宁夏多力新型材料科技有限公司 | Preparation process, equipment and formula of water-based paint |
| CN111110075A (en) * | 2019-12-02 | 2020-05-08 | 斯贝乐电器（浙江）股份有限公司 | Butter making machine |
| CN113153251A (en) * | 2021-02-07 | 2021-07-23 | 胜利油田胜利泵业有限责任公司 | Rotary shearing type polymer viscosity reduction device |
| CN113208093A (en) * | 2021-04-29 | 2021-08-06 | 焙之道食品(福建)有限公司 | Baking-resistant salad sauce preparation system and preparation method |
| CN113303462A (en) * | 2021-04-29 | 2021-08-27 | 焙之道食品(福建)有限公司 | Bread sandwich salad sauce preparation system and method |
| CN113303462B (en) * | 2021-04-29 | 2024-05-17 | 焙之道食品(福建)有限公司 | Bread sandwich salad sauce preparation system |
| CN114471208A (en) * | 2022-01-17 | 2022-05-13 | 河南工业大学 | Preparation facilities of liquid dairy products that contains dietary fiber |
| CN114471208B (en) * | 2022-01-17 | 2022-12-13 | 河南工业大学 | Preparation facilities of liquid dairy products that contains dietary fiber |
| CN114732048A (en) * | 2022-04-25 | 2022-07-12 | 江苏新小莓食品有限公司 | Double-protein milk composite fermentation process |
| CN114732048B (en) * | 2022-04-25 | 2023-11-07 | 江苏新小莓食品有限公司 | Homogenizing device and double-protein-milk composite fermentation process using same |
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